Wet strength resins derived from renewable resources

ABSTRACT

The present invention relates to cationic polymers, such as polyaminoamide epichlorohydrin (PAE), that are derived from renewable resources and can be used to produce wet strength resins suitable for a variety of applications, such as in absorbent paper articles.

FIELD OF THE INVENTION

The present invention relates to cationic polymers (e.g., polyaminoamideepichlorohydrin resins) that are derived from renewable resources andcan be used to produce resins suitable for a variety of applications,such as wet strength additives in absorbent paper articles.

BACKGROUND OF THE INVENTION

The use of disposable products made from webs of paper, such as papertowels, facial tissues, and sanitary tissues, is pervasive in modernindustrialized societies. These products must exhibit certain physicalcharacteristics, such as strength, softness, and absorbency. Strength isthe ability of a paper to retain its physical integrity during use.Softness is the pleasing tactile sensation the user perceives whencontacting or crumpling the paper. Absorbency is the characteristic ofthe paper that allows it to take up and retain certain fluids,particularly water, aqueous solutions, and aqueous suspensions.Absorbency encompasses the absolute quantity of fluid a given amount ofpaper will hold, the rate at which the paper will absorb the fluid and,when the paper is formed into an article (e.g., towel, wipe), theability of the paper to cause a fluid to preferentially be taken up intothe paper and leave a wiped surface dry.

The wet strength of paper can be increased through the incorporation ofan additive that both adheres to the pulp, and forms a network thatrepresses swelling of cellulose fibers, inhibiting the separation offiber-fiber contacts when paper is rewetted. These wet strengthadditives are typically water soluble, cationic polymers that can formcrosslinked networks with themselves or with cellulose. The earliestcationic wet strength resins were condensation products of urea andformaldehyde with small amounts of polyamines

Polyaminoamide epichlorohydrin (PAE) resins were developed as wetstrength resins in the 1950s and 1960s, as described in U.S. Pat. No.2,926,154, incorporated herein by reference. PAE resins are produced bycondensing a polyamine (e.g., diethylenetriamine) with a dibasic acid(e.g., adipic acid) or its ester to form a polyaminoamide.Epichlorohydrin is reacted with the primary and secondary amino groupsof the polyaminoamide to form epoxides and chlorohydrins. At neutral pHand above ambient temperatures, the chlorohydrin groups cyclizespontaneously to form 3-hydroxyazetidinium groups. These strained ringsconfer both reactivity and pH independent cationic charge to the resinmacromolecule. Some of the azetidinium groups crosslink themacromolecules concurrently with the alkylation and cyclizationreactions during resin manufacture, as described in Espy, Tappi J.78(4):90-99. Examples of PAE resins are shown below.

An example of the crosslinking mechanism of a PAE resin is shown below.

The materials used to produce PAE resins (e.g., diethylenetriamine,adipic acid, epichlorohydrin) are derived from non-renewable resources,such as petroleum, natural gas, and coal. As used herein, “renewableresource” refers to one that is produced by a natural process at a ratecomparable to its rate of consumption (e.g., within a 100 year timeframe). The resource can be replenished naturally, or via agriculturaltechniques. Nonlimiting examples of renewable resources include plants(e.g., sugar cane, beets, corn, potatoes, citrus fruit, woody plants,lignocellulosics, hemicellulosics, cellulosic waste), animals, fish,bacteria, fungi, and forestry products. These resources can be naturallyoccurring, hybrids, or genetically engineered organisms. Naturalresources such as crude oil, natural gas, coal, and peat, which takelonger than 100 years to form, are examples of non-renewable resources.As used herein, “petroleum” refers to crude oil and its components ofparaffinic, cycloparaffinic, and aromatic hydrocarbons. Crude oil may beobtained from tar sands, bitumen fields, and oil shale.

Thus, the price and availability of the petroleum, natural gas, and coalfeedstock ultimately have a significant impact on the price of PAEresins. As the worldwide price of petroleum, natural gas, and/or coalescalates, so does the price of PAE resins and articles made using PAEresins, such as paper towels. Furthermore, many consumers display anaversion to purchasing products that are derived from petrochemicals. Insome instances, consumers are hesitant to purchase products made fromlimited non-renewable resources (e.g., petroleum, natural gas, andcoal). Other consumers may have adverse perceptions about productsderived from petrochemicals as being “unnatural” or not environmentallyfriendly.

Accordingly, it would be desirable to provide cationic polymers suitablefor use as wet strength resins using monomers derived from renewableresources, where the resulting polymer has desired performancecharacteristics, such as appropriate wet strength, dry strength, and wetstrength to dry strength ratio with no negative impact on properties,such as paper softness.

SUMMARY OF THE INVENTION

In one aspect, the invention relates to a polymer of Formula I:

-   wherein A is Cl, Br, OH, NO₃, or BF₄;-   each W independently is (CH₂)₁₋₈ or

-   each Y independently is (CH₂)₁₋₈ or

-   each R¹ independently is H,

and each R² is H; or R¹ and R² together with the nitrogen to which theyare attached form

with the proviso that about 20 mole percent to about 40 mole percent ofR¹ are H;

-   each R³ independently is H or OH;-   p is 1-8;-   each q independently is 0-8;-   wherein the molar ratio of W to Y is about 0.8:1 to about 1.4:1;    and,-   wherein Formula I has a biobased content of at least about 95%,    preferably at least about 97%, more preferably at least about 99%.

In another aspect, the invention relates to a method of synthesizing thepolymer of Formula I, wherein the method comprises:

(a) reacting:

-   -   (i)

having a biobased content of at least about 95%; and,

-   -   (ii)

having a biobased content of at least about 95%;

-   -   to form

having a biobased content of at least about 95%; and,

(b) functionalizing the product from step (a)

with having a biobased content of at least about 95%;

-   wherein each W independently is (CH₂)₁₋₈ or

-   each Y independently is (CH₂)₁₋₈ or

-   each Z independently is H or

-   each R³ independently is H or OH;-   p is 1-8;-   each q independently is 0-8; and,-   the molar ratio of W to Y is about 0.8:1 to about 1.4:1.

In yet another aspect, the invention relates to a paper articlecomprising a polymer of Formula I, wherein the paper article has a drystrength of about 300 g/in per ply to about 2000 g/in per ply, and a wetstrength of about 60 g/in per ply to about 400 g/in per ply. In someembodiments, the paper article is selected from the group consisting ofa towel, a tissue (e.g., a facial tissue), and paperboard having singleor multiple ply characteristics.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

A sustainable, wet strength resin has now been found that is entirelyderived from renewable resources. As used herein, “sustainable” refersto a material having an improvement of greater than 10% in some aspectof its Life Cycle Assessment, when compared to similar virgin,petroleum-based material. As used herein, “Life Cycle Assessment” (LCA)or “Life Cycle Inventory” (LCI) refers to the investigation andevaluation of the environmental impacts of a given product or servicecaused or necessitated by its existence. The LCA or LCI can involve a“cradle-to-grave” analysis, which refers to the full Life CycleAssessment or Life Cycle Inventory from manufacture (“cradle”) to usephase and disposal phase (“grave”). All inputs and outputs areconsidered for all the phases of the life cycle. As used herein, “End ofLife” (EoL) scenario refers to the disposal phase of the LCA.Alternatively, LCA can involve a “cradle-to-gate” analysis, which refersto an assessment of a partial product life cycle from manufacture(“cradle”) to the factory gate (i.e., before it is transported to theconsumer) as a pellet.

The renewable wet strength resins of the invention are advantageousbecause they have the same performance characteristics as wet strengthresins made from petroleum-based resources, yet improved sustainability,which reduces dependence on petroleum supplies.

All percentages herein are by weight unless specified otherwise.

Cationic Polymers Comprising Monomers Derived from Renewable Resources

In one aspect, the invention relates to a sustainable, cationic polymerof Formula I:

-   wherein A is Cl, Br, OH, NO₃, or BF₄;-   each W independently is (CH₂)₁₋₈ or

-   each Y independently is (CH₂)₁₋₈ or

-   each R¹ independently is H,

and each R² is H; or R¹ and R² together with the nitrogen to which theyare attached form

with the proviso that about 20 mole percent to about 40 mole percent,preferably about 25 mole percent to about 35 mole percent, for example,about 30 mole percent, of R¹ are H;

-   each R³ independently is H or OH;-   p is 1-8; and,-   each q independently is 0-8.

In some embodiments, the molar ratio of W to Y is about 0.8:1 to about1.4:1, preferably about 0.9:1 to about 1.2:1, for example, about 0.92:1to about 1.14:1

The polymer of Formula I has a biobased content of at least about 95%,preferably at least about 97%, more preferably at least about 99%, forexample, 100%. As used herein, “biobased content” refers to the amountof biobased carbon in a material as a percent of the weight (mass) ofthe total organic carbon in the product. For example, polyethylenecontains two carbon atoms in its structural unit. If ethylene is derivedfrom a renewable resource, then a homopolymer of polyethylenetheoretically has a biobased content of 100% because all of the carbonatoms are derived from a renewable resource. A copolymer of polyethylenecould also theoretically have a biobased content of 100% if both theethylene and the co-monomer are each derived from a renewable resource.As another example, polyethylene terephthalate contains ten carbon atomsin its structural unit (i.e., two carbon atoms from the ethylene glycolmonomer and eight carbon atoms from the terephthalic acid monomer). Ifthe ethylene glycol portion is derived from a renewable resource, butthe terephthalic acid is derived from a petroleum-based resource, thetheoretical biobased content of the polyethylene terephthalate is 20%.

In some embodiments, each W independently is (CH₂)₁₋₈, preferably(CH₂)₂₋₄, for example, (CH₂)₄.

In some embodiments, each Y independently is (CH₂)₁₋₈, preferably(CH₂)_(2-4,) for example, (CH₂)₂.

In some embodiments, p is 1-4, preferably 1-3, for example, 1.

In some preferred embodiments, each A is Cl, each W independently is(CH₂)₄, each Y independently is (CH₂)₂, each R¹ and R² are as describedabove, and p is 1. In some embodiments, the wet strength polymer ispolyetherimide that has been functionalized with epichlorohydrin.

Nonlimiting examples of the wet strength polymer are shown in the belowTable 1, wherein each R¹ and R² are as previously described.

TABLE 1

a b p a b p a b p a b p a b p 1 1 1 1 6 2 1 3 4 1 8 5 1 5 7 2 1 1 2 6 22 3 4 2 8 5 2 5 7 3 1 1 3 6 2 3 3 4 3 8 5 3 5 7 4 1 1 4 6 2 4 3 4 4 8 54 5 7 5 1 1 5 6 2 5 3 4 5 8 5 5 5 7 6 1 1 6 6 2 6 3 4 6 8 5 6 5 7 7 1 17 6 2 7 3 4 7 8 5 7 5 7 8 1 1 8 6 2 8 3 4 8 8 5 8 5 7 1 2 1 1 7 2 1 4 41 1 6 1 6 7 2 2 1 2 7 2 2 4 4 2 1 6 2 6 7 3 2 1 3 7 2 3 4 4 3 1 6 3 6 74 2 1 4 7 2 4 4 4 4 1 6 4 6 7 5 2 1 5 7 2 5 4 4 5 1 6 5 6 7 6 2 1 6 7 26 4 4 6 1 6 6 6 7 7 2 1 7 7 2 7 4 4 7 1 6 7 6 7 8 2 1 8 7 2 8 4 4 8 1 68 6 7 1 3 1 1 8 2 1 5 4 1 2 6 1 7 7 2 3 1 2 8 2 2 5 4 2 2 6 2 7 7 3 3 13 8 2 3 5 4 3 2 6 3 7 7 4 3 1 4 8 2 4 5 4 4 2 6 4 7 7 5 3 1 5 8 2 5 5 45 2 6 5 7 7 6 3 1 6 8 2 6 5 4 6 2 6 6 7 7 7 3 1 7 8 2 7 5 4 7 2 6 7 7 78 3 1 8 8 2 8 5 4 8 2 6 8 7 7 1 4 1 1 1 3 1 6 4 1 3 6 1 8 7 2 4 1 2 1 32 6 4 2 3 6 2 8 7 3 4 1 3 1 3 3 6 4 3 3 6 3 8 7 4 4 1 4 1 3 4 6 4 4 3 64 8 7 5 4 1 5 1 3 5 6 4 5 3 6 5 8 7 6 4 1 6 1 3 6 6 4 6 3 6 6 8 7 7 4 17 1 3 7 6 4 7 3 6 7 8 7 8 4 1 8 1 3 8 6 4 8 3 6 8 8 7 1 5 1 1 2 3 1 7 41 4 6 1 1 8 2 5 1 2 2 3 2 7 4 2 4 6 2 1 8 3 5 1 3 2 3 3 7 4 3 4 6 3 1 84 5 1 4 2 3 4 7 4 4 4 6 4 1 8 5 5 1 5 2 3 5 7 4 5 4 6 5 1 8 6 5 1 6 2 36 7 4 6 4 6 6 1 8 7 5 1 7 2 3 7 7 4 7 4 6 7 1 8 8 5 1 8 2 3 8 7 4 8 4 68 1 8 1 6 1 1 3 3 1 8 4 1 5 6 1 2 8 2 6 1 2 3 3 2 8 4 2 5 6 2 2 8 3 6 13 3 3 3 8 4 3 5 6 3 2 8 4 6 1 4 3 3 4 8 4 4 5 6 4 2 8 5 6 1 5 3 3 5 8 45 5 6 5 2 8 6 6 1 6 3 3 6 8 4 6 5 6 6 2 8 7 6 1 7 3 3 7 8 4 7 5 6 7 2 88 6 1 8 3 3 7 8 4 7 5 6 8 2 8 1 7 1 1 4 3 1 1 5 1 6 6 1 3 8 2 7 1 2 4 32 1 5 2 6 6 2 3 8 3 7 1 3 4 3 3 1 5 3 6 6 3 3 8 4 7 1 4 4 3 4 1 5 4 6 64 3 8 5 7 1 5 4 3 5 1 5 5 6 6 5 3 8 6 7 1 6 4 3 6 1 5 6 6 6 6 3 8 7 7 17 4 3 7 1 5 7 6 6 7 3 8 8 7 1 8 4 3 8 1 5 8 6 6 8 3 8 1 8 1 1 5 3 1 2 51 7 6 1 4 8 2 8 1 2 5 3 2 2 5 2 7 6 2 4 8 3 8 1 3 5 3 3 2 5 3 7 6 3 4 84 8 1 4 5 3 4 2 5 4 7 6 4 4 8 5 8 1 5 5 3 5 2 5 5 7 6 5 4 8 6 8 1 6 5 36 2 5 6 7 6 6 4 8 7 8 1 7 5 3 7 2 5 7 7 6 7 4 8 8 8 1 8 5 3 8 2 5 8 7 68 4 8 1 1 2 1 6 3 1 3 5 1 8 6 1 5 8 2 1 2 2 6 3 2 3 5 2 8 6 2 5 8 3 1 23 6 3 3 3 5 3 8 6 3 5 8 4 1 2 4 6 3 4 3 5 4 8 6 4 5 8 5 1 2 5 6 3 5 3 55 8 6 5 5 8 6 1 2 6 6 3 6 3 5 6 8 6 6 5 8 7 1 2 7 6 3 7 3 5 7 8 6 7 5 88 1 2 8 6 3 8 3 5 8 8 6 8 5 8 1 2 2 1 7 3 1 4 5 1 1 7 1 6 8 2 2 2 2 7 32 4 5 2 1 7 2 6 8 3 2 2 3 7 3 3 4 5 3 1 7 3 6 8 4 2 2 4 7 3 4 4 5 4 1 74 6 8 5 2 2 5 7 3 5 4 5 5 1 7 5 6 8 6 2 2 6 7 3 6 4 5 6 1 7 6 6 8 7 2 27 7 3 7 4 5 7 1 7 7 6 8 8 2 2 8 7 3 8 4 5 8 1 7 8 6 8 1 3 2 1 8 3 1 5 51 2 7 1 7 8 2 3 2 2 8 3 2 5 5 2 2 7 2 7 8 3 3 2 3 8 3 3 5 5 3 2 7 3 7 84 3 2 4 8 3 4 5 5 4 2 7 4 7 8 5 3 2 5 8 3 5 5 5 5 2 7 5 7 8 6 3 2 6 8 36 5 5 6 2 7 6 7 8 7 3 2 7 8 3 7 5 5 7 2 7 7 7 8 8 3 2 8 8 3 8 5 5 8 2 78 7 8 1 4 2 1 1 4 1 6 5 1 3 7 1 8 8 2 4 2 2 1 4 2 6 5 2 3 7 2 8 8 3 4 23 1 4 3 6 5 3 3 7 3 8 8 4 4 2 4 1 4 4 6 5 4 3 7 4 8 8 5 4 2 5 1 4 5 6 55 3 7 5 8 8 6 4 2 6 1 4 6 6 5 6 3 7 6 8 8 7 4 2 7 1 4 7 6 5 7 3 7 7 8 88 4 2 8 1 4 8 6 5 8 3 7 8 8 8 1 5 2 1 2 4 1 7 5 1 4 7 2 5 2 2 2 4 2 7 52 4 7 3 5 2 3 2 4 3 7 5 3 4 7 4 5 2 4 2 4 4 7 5 4 4 7 5 5 2 5 2 4 5 7 55 4 7 6 5 2 6 2 4 6 7 5 6 4 7 7 5 2 7 2 4 7 7 5 7 4 7 8 5 2 8 2 4 8 7 58 4 7

Additional nonlimiting examples of the wet strength polymer are shown inthe below Table 2, wherein each R¹ and R² are as previously described.

TABLE 2

b p q q′ q″ R³ R^(3′) R^(3″) b p q q′ q″ R³ R^(3′) R^(3″) 1 1 1 1 0 H HH 1 5 1 1 0 H H H 2 1 1 1 0 H H H 2 5 1 1 0 H H H 3 1 1 1 0 H H H 3 5 11 0 H H H 4 1 1 1 0 H H H 4 5 1 1 0 H H H 5 1 1 1 0 H H H 5 5 1 1 0 H HH 6 1 1 1 0 H H H 6 5 1 1 0 H H H 7 1 1 1 0 H H H 7 5 1 1 0 H H H 8 1 11 0 H H H 8 5 1 1 0 H H H 1 1 1 1 0 H H OH 1 5 1 1 0 H H OH 2 1 1 1 0 HH OH 2 5 1 1 0 H H OH 3 1 1 1 0 H H OH 3 5 1 1 0 H H OH 4 1 1 1 0 H H OH4 5 1 1 0 H H OH 5 1 1 1 0 H H OH 5 5 1 1 0 H H OH 6 1 1 1 0 H H OH 6 51 1 0 H H OH 7 1 1 1 0 H H OH 7 5 1 1 0 H H OH 8 1 1 1 0 H H OH 8 5 1 10 H H OH 1 1 1 1 0 OH H H 1 5 1 1 0 OH H H 2 1 1 1 0 OH H H 2 5 1 1 0 OHH H 3 1 1 1 0 OH H H 3 5 1 1 0 OH H H 4 1 1 1 0 OH H H 4 5 1 1 0 OH H H5 1 1 1 0 OH H H 5 5 1 1 0 OH H H 6 1 1 1 0 OH H H 6 5 1 1 0 OH H H 7 11 1 0 OH H H 7 5 1 1 0 OH H H 8 1 1 1 0 OH H H 8 5 1 1 0 OH H H 1 2 1 10 H H H 1 6 1 1 0 H H H 2 2 1 1 0 H H H 2 6 1 1 0 H H H 3 2 1 1 0 H H H3 6 1 1 0 H H H 4 2 1 1 0 H H H 4 6 1 1 0 H H H 5 2 1 1 0 H H H 5 6 1 10 H H H 6 2 1 1 0 H H H 6 6 1 1 0 H H H 7 2 1 1 0 H H H 7 6 1 1 0 H H H8 2 1 1 0 H H H 8 6 1 1 0 H H H 1 2 1 1 0 H H OH 1 6 1 1 0 H H OH 2 2 11 0 H H OH 2 6 1 1 0 H H OH 3 2 1 1 0 H H OH 3 6 1 1 0 H H OH 4 2 1 1 0H H OH 4 6 1 1 0 H H OH 5 2 1 1 0 H H OH 5 6 1 1 0 H H OH 6 2 1 1 0 H HOH 6 6 1 1 0 H H OH 7 2 1 1 0 H H OH 7 6 1 1 0 H H OH 8 2 1 1 0 H H OH 86 1 1 0 H H OH 1 2 1 1 0 OH H H 1 6 1 1 0 OH H H 2 2 1 1 0 OH H H 2 6 11 0 OH H H 3 2 1 1 0 OH H H 3 6 1 1 0 OH H H 4 2 1 1 0 OH H H 4 6 1 1 0OH H H 5 2 1 1 0 OH H H 5 6 1 1 0 OH H H 6 2 1 1 0 OH H H 6 6 1 1 0 OH HH 7 2 1 1 0 OH H H 7 6 1 1 0 OH H H 8 2 1 1 0 OH H H 8 6 1 1 0 OH H H 13 1 1 0 H H H 1 7 1 1 0 H H H 2 3 1 1 0 H H H 2 7 1 1 0 H H H 3 3 1 1 0H H H 3 7 1 1 0 H H H 4 3 1 1 0 H H H 4 7 1 1 0 H H H 5 3 1 1 0 H H H 57 1 1 0 H H H 6 3 1 1 0 H H H 6 7 1 1 0 H H H 7 3 1 1 0 H H H 7 7 1 1 0H H H 8 3 1 1 0 H H H 8 7 1 1 0 H H H 1 3 1 1 0 H H OH 1 7 1 1 0 H H OH2 3 1 1 0 H H OH 2 7 1 1 0 H H OH 3 3 1 1 0 H H OH 3 7 1 1 0 H H OH 4 31 1 0 H H OH 4 7 1 1 0 H H OH 5 3 1 1 0 H H OH 5 7 1 1 0 H H OH 6 3 1 10 H H OH 6 7 1 1 0 H H OH 7 3 1 1 0 H H OH 7 7 1 1 0 H H OH 8 3 1 1 0 HH OH 8 7 1 1 0 H H OH 1 3 1 1 0 OH H H 1 7 1 1 0 OH H H 2 3 1 1 0 OH H H2 7 1 1 0 OH H H 3 3 1 1 0 OH H H 3 7 1 1 0 OH H H 4 3 1 1 0 OH H H 4 71 1 0 OH H H 5 3 1 1 0 OH H H 5 7 1 1 0 OH H H 6 3 1 1 0 OH H H 6 7 1 10 OH H H 7 3 1 1 0 OH H H 7 7 1 1 0 OH H H 8 3 1 1 0 OH H H 8 7 1 1 0 OHH H 1 4 1 1 0 H H H 1 8 1 1 0 H H H 2 4 1 1 0 H H H 2 8 1 1 0 H H H 3 41 1 0 H H H 3 8 1 1 0 H H H 4 4 1 1 0 H H H 4 8 1 1 0 H H H 5 4 1 1 0 HH H 5 8 1 1 0 H H H 6 4 1 1 0 H H H 6 8 1 1 0 H H H 7 4 1 1 0 H H H 7 81 1 0 H H H 8 4 1 1 0 H H H 8 8 1 1 0 H H H 1 4 1 1 0 H H OH 1 8 1 1 0 HH OH 2 4 1 1 0 H H OH 2 8 1 1 0 H H OH 3 4 1 1 0 H H OH 3 8 1 1 0 H H OH4 4 1 1 0 H H OH 4 8 1 1 0 H H OH 5 4 1 1 0 H H OH 5 8 1 1 0 H H OH 6 41 1 0 H H OH 6 8 1 1 0 H H OH 7 4 1 1 0 H H OH 7 8 1 1 0 H H OH 8 4 1 10 H H OH 8 8 1 1 0 H H OH 1 4 1 1 0 OH H H 1 8 1 1 0 OH H H 2 4 1 1 0 OHH H 2 8 1 1 0 OH H H 3 4 1 1 0 OH H H 3 8 1 1 0 OH H H 4 4 1 1 0 OH H H4 8 1 1 0 OH H H 5 4 1 1 0 OH H H 5 8 1 1 0 OH H H 6 4 1 1 0 OH H H 6 81 1 0 OH H H 7 4 1 1 0 OH H H 7 8 1 1 0 OH H H 8 4 1 1 0 OH H H 8 8 1 10 OH H H

In another aspect, the invention relates to a method for synthesizingthe polymer of Formula I, wherein the method comprises:

-   (a) reacting:

compound (i):

and

compound (ii):

to form compound (iii):

and,

-   (b) functionalizing compound (iii) with

-   wherein each W independently is (CH₂)₁₋₈ or

-   each Y independently is (CH₂)₁₋₈ or

-   each Z independently is H or

-   each R³ independently is H or OH;-   p is 1-8; and,-   each q independently is 0-8;-   wherein compounds (i), (ii), and (iii) each have a biobased content    of at least about 95%, preferably about 97%, more preferably about    99%, for example, about 100%.

In some embodiments, the molar ratio of W to Y is about 0.8:1 to about1.4:1, preferably about 0.9:1 to about 1.2:1, for example, about 0.92:1to about 1.14:1.

In some embodiments, each W independently is (CH₂)₁₋₈, preferably(CH₂)₂₋₄, for example, (CH₂)₄. In some embodiments, compound (i) is adicarboxylic acid or tricarboxylic acid selected from the groupconsisting of malonic acid, succinic acid, glutaric acid, adipic acid,pimelic acid, suberic acid, azelaic acid, sebacic acid, citric acid,isocitric acid, propane-1,2,3-dicarboxylic acid, and mixtures thereof.In some preferred embodiments, compound (i) is selected from the groupconsisting of malonic acid, succinic acid, glutaric acid, adipic acid,and mixtures thereof. For example, compound (i) is adipic acid.

In some embodiments, each Y independently is (CH₂)₁₋₈, preferably(CH₂)₂₋₄, for example, (CH₂)₂, and p is 1-4, preferably 1-3, forexample, 1. In some embodiments, compound (ii) is a polyalkylenepolyamine having two primary amines and at least one secondary amine. Insome embodiments, compound (ii) is selected from the group consisting ofdiethylenetriamine, triethylenetetramine, tetraethylenepentamine,dipropylenetriamine, and mixtures thereof. In some preferredembodiments, compound (ii) is diethylenetriamine.

Derivation of Monomers from Renewable Resources

The sustainable cationic polymers of the invention are derived fromrenewable resources. In some embodiments, the sustainable cationicpolymer can be formed by reacting a renewable polyalkylene polyaminewith a renewable dicarboxylic or a renewable tricarboxylic acid to forma renewable polyamide, and then functionalizing the renewable polyamidewith renewable epichlorohydrin to form a renewable wet strength cationicpolymer. In some embodiments, the wet strength polymer is renewablepolyetherimide that has been functionalized with renewableepicholorohydrin.

Many of the renewable monomers of the invention are derived frombio-ethylene, bio-propylene, or bio-alcohols derived from renewableresources. As used herein, the prefix “bio-” is used to designate amaterial that has been derived from a renewable resource.

Bio-Alcohol Production

Monofunctional alcohols, such as methanol; ethanol; isomers of propanol,butanol, pentanol, and hexanol; cyclopentanol; isobornyl alcohol; andhigher alcohols; and polyfunctional alcohols, such as ethylene glycol,isomers of propanediol, and glycerol, can be derived from renewableresources via a number of suitable routes (see, e.g., WO 2009/155086 andU.S. Pat. No. 4,536,584, each incorporated herein by reference).

In one route, a renewable resource, such as corn starch, can beenzymatically hydrolyzed to yield glucose and/or other sugars. Theresultant sugars can be converted into alcohols by fermentation.

In another route, monofunctional alcohols, such as ethanol and propanolare produced from short chain acids, fatty acids, fats (e.g., animalfat), and oils (e.g., monoglycerides, diglycerides, triglycerides, andmixtures thereof). These short chain acids, fatty acids, fats, and oilscan be derived from renewable resources, such as animals or plants.“Short chain acid” refers to a straight chain monocarboyxlic acid havinga chain length of 3 to 5 carbon atoms. “Fatty acid” refers to a straightchain monocarboxylic acid having a chain length of 6 to 30 carbon atoms.“Monoglycerides,” “diglycerides,” and “triglycerides” refer to multiplemono-, di- and tri-esters, respectively, of (i) glycerol and (ii) thesame or mixed short chain acids and/or fatty acids.

Nonlimiting examples of short chain acids include propionic acid,butyric acid, and valeric acid. Nonlimiting examples of saturated fattyacids include caproic acid, enanthic acid, caprylic acid, pelargonicacid, capric acid, undecylic acid, lauric acid, tridecylic acid,myristic acid, pentadecylic acid, palmitic acid, margaric acid, stearicacid, nonadecylic acid, arachidic acid, heneicosylic acid, behenic acid,tricosylic acid, lignoceric acid, pentacosylic acid, cerotic acid,heptacosylic acid, montanic acid, nonacoxylic acid, melissic acid,henatriacontylic acid, lacceroic acid, psyllic acid, geddic acid,ceroplastic acid, and hexatriacontylic acid. Nonlimiting examples ofunsaturated fatty acids include oleic acid, myristoleic acid,palmitoleic acid, sapienic acid, linoleic acid, linolenic acid,arachidonic acid, eicosapentaenoic acid, and docosahexaenoic acid.Nonlimiting examples of monoglycerides include monoglycerides of any ofthe fatty acids described herein. Nonlimiting examples of diglyceridesinclude diglycerides of any of the fatty acids described herein.Nonlimiting examples of the triglycerides include triglycerides of anyof the fatty acids described herein, such as, for example, tall oil,corn oil, soybean oil, sunflower oil, safflower oil, linseed oil,perilla oil, cotton seed oil, tung oil, peanut oil, oiticica oil,hempseed oil, marine oil (e.g. alkali-refined fish oil), dehydratedcastor oil, and mixtures thereof. Alcohols can be produced from fattyacids through reduction of the fatty acids by any method known in theart. Alcohols can be produced from fats and oils by first hydrolyzingthe fats and oils to produce glycerol and fatty acids, and thensubsequently reducing the fatty acids.

In another route, genetically engineered cells and microorganisms areprovided that produce products from the fatty acid biosynthetic pathway(i.e., fatty acid derivatives), such as fatty alcohols, as described inInternational Patent Application Publication No. WO 2008/119082,incorporated herein by reference. For example, a gene encoding a fattyalcohol biosynthetic polypeptide that can be used to produce fattyalcohols, or a fatty aldehyde biosynthetic polypeptide that can be usedto produce fatty aldehydes, which subsequently can be converted to fattyalcohols, is expressed in a host cell. The resulting fatty alcohol orfatty aldehyde then is isolated from the host cell. Such methods aredescribed in U.S. Patent Application Publication Nos. 2010/0105963 and2010/0105955, and International Patent Application Publication Nos. WO2010/062480 and WO 2010/042664, each incorporated herein by reference.

In another route, fatty acyl chains are produced from renewable biocrudeor hydrocarbon feedstocks using recombinant microorganisms, wherein atleast one hydrocarbon is produced by the recombinant microorganism. Thefatty acyl chains subsequently can be converted to fatty alcohols usingmethods known in the art. The microorganisms can be engineered toproduce specific degrees of branching, saturation, and length, asdescribed in U.S. Patent Application Publication No. 2010/017826,incorporated herein by reference.

Bio-Ethylene Production

Bio-ethylene can be formed from the dehydration of bio-ethanolBio-ethanol can be derived from, for example, (i) the fermentation ofsugar from sugar cane, sugar beet, or sorghum; (ii) the saccharificationof starch from maize, wheat, or manioc; and (iii) the hydrolysis ofcellulosic materials. U.S. Patent Application Publication No.2005/0272134, incorporated herein by reference, describes thefermentation of sugars to form alcohols and acids.

As previously described, suitable sugars used to form ethanol includemonosaccharides, disaccharides, trisaccharides, and oligosaccharides.Sugars, such as sucrose, glucose, fructose, and maltose, are readilyproduced from renewable resources, such as sugar cane and sugar beets.Sugars also can be derived (e.g., via enzymatic cleavage) from otheragricultural products (i.e., renewable resources resulting from thecultivation of land or the husbandry of animals). For example, glucosecan be prepared on a commercial scale by enzymatic hydrolysis of cornstarch. Other common agricultural crops that can be used as the basestarch for conversion into glucose include wheat, buckwheat, arracaha,potato, barley, kudzu, cassava, sorghum, sweet potato, yam, arrowroot,sago, and other like starchy fruit, seeds, or tubers. The sugarsproduced by these renewable resources (e.g., corn starch from corn) canbe used to produce ethanol, as well as other alcohols, such as propanol,and methanol. For example, corn starch can be enzymatically hydrolyzedto yield glucose and/or other sugars. The resultant sugars can beconverted into ethanol by fermentation.

In one embodiment, bio-ethylene is produced from sugar cane. The lifecycle stages of ethylene production from sugar cane include (i) sugarcane farming, (ii) fermentation of sugar cane to form bio-ethanol, and(iii) dehydration of bio-ethanol to form ethylene. Specifically, sugarcane is washed and transported to mills where sugar cane juice isextracted, leaving filter cake, which is used as fertilizer, and bagasse(residual woody fiber of the cane obtained after crushing). The bagasseis burned to generate steam and the electricity used to power the sugarcane mills, thereby reducing the use of petroleum-derived fuels. Thesugar cane juice is fermented using yeast to form a solution of ethanoland water. The ethanol is distilled from the water to yield about 95%pure bio-ethanol. The bio-ethanol is subjected to catalytic dehydration(e.g., with an alumina catalyst) to produce bio-ethylene.

Advantageously, a Life Cycle Assessment and Inventory of ethyleneproduced from sugar cane shows favorable benefits in some aspects overethylene produced from petroleum feedstock for global warming potential,abiotic depletion, and fossil fuel consumption. For example, somestudies have shown that about one ton of polyethylene made from virginpetroleum-based sources results in the emission of up to about 2.5 tonsof carbon dioxide to the environment, as previously described. Thus, useof up to about one ton of polyethylene from a renewable resource, suchas sugar cane, results in a decrease of about 5 tons of environmentalcarbon dioxide versus using one ton of polyethylene derived frompetroleum-based resources.

Bio-Propylene

Bio-propylene can be formed from the dehydration of bio-propanol.Renewable resources used to derive bio-propanol are as previouslydescribed. Bio-propanol also can be derived from bio-ethylene. In thispathway, bio-ethylene is converted into bio-propionaldehyde byhydroformylation using carbon monoxide and hydrogen in the presence of acatalyst, such as cobalt octacarbonyl or a rhodium complex.Hydrogenation of the bio-propionaldehyde in the presence of a catalyst,such as sodium borohydride and lithium aluminum hydride, yieldsbio-propan-1-ol, which can be dehydrated in an acid catalyzed reactionto yield bio-propylene, as described in U.S. Patent ApplicationPublication No. 2007/0219521, incorporated herein by reference.

A. Dicarboxylic Acid

The dicarboxylic acid derived from renewable resources can berepresented by compound (i):

-   wherein each W independently is (CH₂)₁₋₈ or

-   each R³ independently is H or OH; and,-   each q independently is 0-8.

Bio-Malonic Acid

In some embodiments, compound (i) is bio-malonic acid. In one route,bio-malonic acid can be produced by first oxidizing bio-ethylene in thepresence of a silver catalyst to form bio-ethylene oxide, whichundergoes hydroformylation to produce bio-3-hydroxypropionaldehyde. Thebio-3-hydroxypropionaldehyde is hydrogenated to frombio-1,3-propanediol, which is oxidized using methods known to oneskilled in the art to form bio-malonic acid.

In another route, the bio-1,3-propanediol can be produced through thefermentation of glycerol using Clostridium bacteria (e.g., Clostridiumdiolis). As previously described, glycerol can be obtained from fattyacids, fats, and oils.

In yet another route, the bio-1,3-propanediol can be produced throughthe conversion of corn syrup effected by a genetically modified strainof E. coli.

Bio-Succinic Acid

In some embodiments, compound (i) is bio-succinic acid. Bio-succinicacid is a by-product of sugar fermentation. It also can be produced byoxidizing bio-1,4-butanediol, according to methods known to one skilledin the art.

In one route, bio-ethylene is first converted to bio-acetylene. Thebio-acetylene is reacted with two equivalents of bio-formaldehyde toform bio-1,4-butynediol, which is hydrogenated to producebio-1,4-butanediol. Bio-formaldehyde can be produced through thecatalytic oxidation of bio-methanol using silver metal or a mixture ofiron and molybdenum or vanadium oxides.

In another route, bio-propylene oxide or bio-propanol is converted tobio-allyl alcohol by isomerization or dehydration, respectively. Thebio-allyl alcohol is hydroformylated to form bio-4-hydroxybutyraldehyde,which is reduced to bio-1,4-butanediol. The bio-propylene oxide can besynthesized by the oxidation of bio-propylene using H₂O₂, or byconverting bio-propylene to bio-1-chloro-2-propanol andbio-2-chloro-1-propanol using chlorine and water, and then reacting thebio-chloropropanols with hydroxide to form bio-propylene oxide.

In yet another route, the bio-1,4-butanediol can be produced through themetabolization of sugar by a genetically modified strain of E. coli.

Bio-Glutaric Acid

In some embodiments, compound (i) is bio-glutaric acid. Bio-glutaricacid can be produced by the ring opening of bio-butyrolactone usingpotassium bio-cyanide to result in potassium bio-carboxylate-nitrile,which is hydrolyzed to bio-glutaric acid. Potassium bio-cyanide can beproduced from the reaction of KOH with bio-hydrogen cyanide.Bio-hydrogen cyanide can be produced by reacting bio-methane withammonia. Bio-butyrolactone can be produced by removing water frombio-γ-hydroxybutryic acid, which can be produced frombio-1,4-butanediol.

In another route, bio-glutaric acid is produced by reactingbio-1,3-dibromopropane with bio-sodium or bio-potassium cyanide to formthe bio-dinitrile, which can undergo hydrolysis to form bio-glutaricacid. The bio-1,3-dibromopropane can be formed by free radical additionbetween bio-allyl bromide with HBr.

Bio-Adipic Acid

In some embodiments, compound (i) is bio-adipic acid. Bio-adipic acidcan be produced from the oxidation of fats, using methods known to oneskilled in the art. Bio-adipic acid can also be produced through thecarbonylation of bio-butadiene using two equivalents of carbon dioxideand two equivalents of water. Bio-butadiene can be produced frombio-ethanol either using a metal oxide catalyst in a one-step process at400-450° C., or oxidizing the bio-ethanol to bio-acetaldehyde, whichreacts with additional bio-ethanol over a tantalum-promoted poroussilica catalyst at 325 ° C. to 350° C.

Bio-Pimelic Acid, Bio-Suberic Acid, and Bio-Azelaic Acid

In some embodiments, compound (i) is bio-pimelic acid, bio-suberic acid,or bio-azelaic acid, all of which can be produced from the oxidation offats produced from ricinoleic acid, which can be obtained from castoroil. In some embodiments, the double bond of ricinoleic acid is splitinto bio-suberic acid and bio-azelaic acid. Bio-azelaic acid also can beproduced from the oxidation of oleic acid with potassium permanganate,or the oxidative cleavage of oleic acid with chromic acid or usingozonolysis.

Bio-Sebacic Acid

In some embodiments, compound (i) is bio-sebacic acid. Bio-sebacic acidcan be isolated from beef tallow. Bio-sebacic acid can also be producedby the treatment of ricinoleic acid with sodium hydroxide, as describedin U.S. Patent Application Publication No. 2010/0151241, incorporatedherein by reference.

Bio-Citric Acid and Bio-Isocitric Acid

In some embodiments, compound (i) is bio-citric acid or bio-isocitricacid, both of which are naturally occurring tricarboxylic acids.

Bio-Propane-1,2,3-Tricarboxylic Acid

In some embodiments, compound (i) is bio-propane-1,2,3-tricarboxylicacid. Bio-propane-1,2,3-tricarboxylic acid is naturally occurring. Itcan also be produced from bio-fumaric acid in two steps. Bio-fumaricacid can be produced from bio-succinic acid.

B. Polyalkylene Polyamine

The polyalkylene polyamine derived from renewable resources can berepresented by compound (ii):

-   wherein each Y independently is (CH₂)₁₋₈ or

-   each Z independently is H or

and

-   p is 1-8.

Bio-Diethylenetriamine, Bio-Triethylenetetramine,Bio-Tetraethylenepentamine

In some embodiments, compound (ii) is bio-diethylenetriamine,bio-triethylenetetramine, bio-tetraethylenepentamine, or a mixturethereof. In one route, bio-diethylenetriamine, biotriethylenetetramine,and bio-tetraethylenepentamine can be produced by reactingbio-dichloroethane with ammonia. Bio-dichloroethane can be produced bychlorinating bio-ethylene.

In another route, bio-diethylenetriamine, bio-triethylenetetramine, andbio-tetraethylenepentamine can be produced by reactingbio-monoethanolamine with ammonia. Bio-monoethanolamine can be producedby reacting bio-ethylene oxide with ammonia. Bio-ethylene oxide can besynthesized as previously described.

In yet another route, bio-diethylenetriamine, bio-triethylenetetramine,and bio-tetraethylenepentamine can be produced by reactingbio-diaminoethane with bio-monoethanolamine. Bio-diaminoethane can besynthesized through the reaction of bio-ethylene glycol, orbio-dichloroethane, or bio-monoethanolamine with ammonia.

Bio-Dipropylenetriamine

In some embodiments, compound (ii) is bio-dipropylenetriamine.Bio-dipropylenetriamine can be produce by reactingbio-1,3-dichloropropane with ammonia. Bio-1,3-dichloropropane can besynthesized by chlorinating bio-propylene to formbio-1,3-dichloropropene, and then reducing the bio-1,3-dichloropropene.

In another route, bio-dipropylenetriamine can be prepared by reactingbio-3-aminopropanol with ammonia. Bio-3-aminopropanol can be synthesizedby reacting bio-acrylonitrile with water. Bio-acrylonitrile can beprepared by reacting bio-propylene with ammonia and molecular oxygen.

In yet another route, bio-dipropylenetriamine can be prepared byreacting bio-acrylonitrile with ammonia to form bio-1,3-propanediamine,and then reacting the bio-1,3-propanediamine with bio-monopropanolamine.

C. Bio-Epichlorohydrin

Bio-epichlorhydrin can be produced from bio-allyl chloride. Bio-allylchloride can be produced by reacting bio-propylene with chlorine at hightemperature (e.g., 500° C.) with the release of hydrochloric acid. Inone route, bio-allyl chloride is hydrochlorinated using hypochlorus acidto form a mixture of 2,3-dichloro-1-propanol and1,3-dichloro-2-propanol. Sodium hydroxide is added to this mixture toproduce bio-epichlorohydrin, sodium chloride, and water. In anotherroute, bio-allyl chloride is hypochlorinated in a dilute, aqueouschlorine solution to form the bio-dichlorohydrins, which are thendehydrochlorinated using either calcium hydroxide or sodium hydroxide toform bio-ephichlorohydrin. In yet another route, bio-allyl chloride isepoxidated using aqueous hydrogen peroxide and aheteropolyphosphatotungstate catalyst to yield bio-epichlorohydrin.

Bio-epichlorohydrin also can be produced from bio-allyl alcohol byreacting the bio-allyl alcohol with chlorine and calcium hydroxide, aspreviously described. Bio-allyl alcohol can be produced by thehydrolysis of bio-allyl chloride, or by the isomerization ofbio-propylene oxide using a potassium alum catalyst at hightemperatures. Bio-allyl alcohol also can be produced through theacetoxylation of bio-propene to form bio-allyl acetate, which can behydrolyzed to yield bio-allyl alcohol. Bio-allyl alcohol also can beproduced by oxidizing bio-propylene to bio-acrolein, and thenhydrogenating the bio-acrolein to form bio-allyl alcohol.

Assessment of the Biobased Content of Materials

A suitable method to assess materials derived from renewable resourcesis through ASTM D6866, which allows the determination of the biobasedcontent of materials using radiocarbon analysis by accelerator massspectrometry, liquid scintillation counting, and isotope massspectrometry. When nitrogen in the atmosphere is struck by anultraviolet light produced neutron, it loses a proton and forms carbonthat has a molecular weight of 14, which is radioactive. This ¹⁴C isimmediately oxidized into carbon dioxide, which represents a small, butmeasurable fraction of atmospheric carbon. Atmospheric carbon dioxide iscycled by green plants to make organic molecules during the processknown as photosynthesis. The cycle is completed when the green plants orother forms of life metabolize the organic molecules producing carbondioxide, which causes the release of carbon dioxide back to theatmosphere. Virtually all forms of life on Earth depend on this greenplant production of organic molecules to produce the chemical energythat facilitates growth and reproduction. Therefore, the ¹⁴C that existsin the atmosphere becomes part of all life forms and their biologicalproducts. These renewably based organic molecules that biodegrade tocarbon dioxide do not contribute to global warming because no netincrease of carbon is emitted to the atmosphere. In contrast, fossilfuel-based carbon does not have the signature radiocarbon ratio ofatmospheric carbon dioxide. See WO 2009/155086, incorporated herein byreference.

The application of ASTM D6866 to derive a “biobased content” is built onthe same concepts as radiocarbon dating, but without use of the ageequations. The analysis is performed by deriving a ratio of the amountof radiocarbon (¹⁴C) in an unknown sample to that of a modern referencestandard. The ratio is reported as a percentage with the units “pMC”(percent modern carbon). If the material being analyzed is a mixture ofpresent day radiocarbon and fossil carbon (containing no radiocarbon),then the pMC value obtained correlates directly to the amount of biomassmaterial present in the sample.

The modern reference standard used in radiocarbon dating is a NIST(National Institute of Standards and Technology) standard with a knownradiocarbon content equivalent approximately to the year AD 1950. Theyear AD 1950 was chosen because it represented a time prior tothermo-nuclear weapons testing, which introduced large amounts of excessradiocarbon into the atmosphere with each explosion (termed “bombcarbon”). The AD 1950 reference represents 100 pMC.

“Bomb carbon” in the atmosphere reached almost twice normal levels in1963 at the peak of testing and prior to the treaty halting the testing.Its distribution within the atmosphere has been approximated since itsappearance, showing values that are greater than 100 pMC for plants andanimals living since AD 1950. The distribution of bomb carbon hasgradually decreased over time, with today's value being near 107.5 pMC.As a result, a fresh biomass material, such as corn, could result in aradiocarbon signature near 107.5 pMC.

Petroleum-based carbon does not have the signature radiocarbon ratio ofatmospheric carbon dioxide. Research has noted that fossil fuels andpetrochemicals have less than about 1 pMC, and typically less than about0.1 pMC, for example, less than about 0.03 pMC. However, compoundsderived entirely from renewable resources have at least about 95 percentmodern carbon (pMC), preferably at least about 99 pMC, for example,about 100 pMC.

Combining fossil carbon with present day carbon into a material willresult in a dilution of the present day pMC content. By presuming that107.5 pMC represents present day biomass materials and 0 pMC representspetroleum derivatives, the measured pMC value for that material willreflect the proportions of the two component types. A material derived100% from present day soybeans would give a radiocarbon signature near107.5 pMC. If that material was diluted with 50% petroleum derivatives,it would give a radiocarbon signature near 54 pMC.

A biobased content result is derived by assigning 100% equal to 107.5pMC and 0% equal to 0 pMC. In this regard, a sample measuring 99 pMCwill give an equivalent biobased content result of 93%.

Assessment of the materials described herein were done in accordancewith ASTM D6866, particularly with Method B. The mean values quoted inthis report encompasses an absolute range of 6% (plus and minus 3% oneither side of the biobased content value) to account for variations inend-component radiocarbon signatures. It is presumed that all materialsare present day or fossil in origin and that the desired result is theamount of biobased component “present” in the material, not the amountof biobased material “used” in the manufacturing process.

Other techniques for assessing the biobased content of materials aredescribed in U.S. Pat. Nos. 3,885,155, 4,427,884, 4,973,841, 5,438,194,and 5,661,299, and WO 2009/155086, each incorporated herein byreference.

Method of Making Wet Strength Resin

The polymers of Formula I can be prepared by condensing a polyalkyleneamine with a dicarboxylic acid, or any active derivative thereof, toform a polyamide, and then reacting the polyamide with epichlorohydrin,as described in, e.g., U.S. Pat. No. 2,926,154.

Condensation of the Polyalkylene Amide with the Dicarboxylic Acid

The condensation of the polyalkylene amine with the dicarboxylic acid toform the polyamide of the invention can occur by any method known to oneskilled in the art, and the reaction parameters used for thiscondensation reaction depend on the exact reaction conditions, asunderstood to one skilled in the art. For example, the reactiontemperature can be about 110° C. to about 250° C. or higher atatmospheric pressure, preferably about 160° C. to about 210° C. Underreduced pressure conditions, the temperature of the condensation alsocan be reduced accordingly. The reaction time depends on the exactreaction conditions and occurs until a substantial amount of startingmaterials have been converted to polyamide, e.g., about 30 minutes toabout 2 hours.

The amount of dicarboxylic acid used should be sufficient to react withsubstantially all of the primary amine groups of the polyalkylenepolyamine, but insufficient to react with the secondary amine groups ofthe polyalkylene polyamine. For example, the ratio of dicarboxylic acidto polyalkylene amine can be about 0.8:1 to about 1.4:1, preferablyabout 0.9:1 to about 1.2:1, more preferably about 0.92:1 to about1.14:1. Ratios below about 0.8:1 result in a gelled product, whileratios above about 1.4:1 result in low molecular weight polyamides. Thecomposition of the polyamide polymer and the ratio of dicarboxylic acidto polyalkylene amine in the polymer can be determined using nuclearmagnetic resonance and_gas chromatography, and by other characterizationmethods known to one skilled in the art.

The molecular weight of the polyalkylene amide can be about 5,000 toabout 30,000, for example, about 10,000. “Molecular weight” as usedherein means “weight average molecular weight.” “Weight averagemolecular weight” means the weight average molecular weight asdetermined using gel permeation chromatography according to the protocolfound in Colloids and Surfaces A. Physico Chemical & EngineeringAspects, Vol. 162, 2000, pg. 107-121.

Functionalization of Polyamide with Epichlorohydrin

The polyamide can be functionalized with epichlorohydrin by any methodknown to one skilled in the art, and the reaction parameters used forthis functionalization depend on the exact reaction conditions, asunderstood to one skilled in the art. In some embodiments, the reactioncan occur in an aqueous solution. Optionally, base can be added to thereaction solution to neutralize some of the acid that forms during theprevious polymerization reaction.

For example, the epichlorohydrin can be reacted with the polyamide at atemperature of about 45° C. to about 100° C., preferably about 45° C. toabout 70° C., until the viscosity of a 20% solids solution at 25° C. hasreached about C or higher on the Gardner-Holdt scale. After the reactionsolution reaches the desired viscosity, sufficient water is added toadjust the solids content of the solution to about 15% or less. Theproduct is cooled to about 25° C., and then stabilized by addingsufficient acid (e.g., hydrochloric acid, sulfuric acid, nitric acid,formic acid, phosphoric acid, acetic acid) to reduce the pH to at leastabout 6, preferably to at least about 5.

In the polyamide-epichlorohydrin reaction, sufficient epichlorohydrinshould be used to convert all secondary amide groups to tertiary aminegroups and/or quaternary ammonium groups, including cyclic structures.However, more or less epichlorohydrin can be added to the polyamide tomoderate or increase reaction rates. For example, about 0.5 mol to about1.8 mol, preferably about 0.9 mol to about 1.5 mol, of epichlorohydrinper mole of polyamide secondary amine is contemplated.

The composition of the polyaminoamide epichlorohydrin resin and theamount of epichlorohydrin functionalization on the polyamide can bedetermined using nuclear magnetic resonance, gas chromatography, and byother characterization methods known to one skilled in the art.

The molecular weight of the polyaminoamide epichlorohydrin resin can becan be about 5,000 to about 30,000, for example, about 10,000.“Molecular weight” as used herein means “weight average molecularweight.” “Weight average molecular weight” means the weight averagemolecular weight as determined using gel permeation chromatographyaccording to the protocol found in Colloids and Surfaces A. PhysicoChemical & Engineering Aspects, Vol. 162, 2000, pg. 107-121.

Paper Article Comprised of Wet Strength Resins Derived from RenewableResources

The invention also relates to a paper article comprising the polymer ofFormula I, as previously described herein. The paper article can be anypaper that used for absorbent purposes (e.g., a towel, a facial tissue,a sanitary tissue, and paperboard. Nonlimiting examples of paperarticles include bath towels, facial tissue, industrial wipers, Kleenex,kraft paper, napkins, paper coveralls, plates, tablecloth covers, toiletseat covers, towels, white butcher paper, C-fold towers, householdtowels, multi-fold towels, roll towels, single fold towels. Additionalexamples of paper articles include airmail papers, artboards, artistspapers, baking paper, blotting papers, book binding materials, bookcover material, book end papers, book papers, bookjacket papers, bulkybook papers, business papers, carbonless papers, carbonless reels,carbonless sheets, cardstock, cartonboards, cast coated papers, checkpapers, cigarette papers, colored papers, copier papers, copier/laserpaper, corrugating medium, cover papers, cupstock, diazo paper, digitalpapers, directory papers, display boards, document/presentation papers,drawing office papers, duplicator papers, electrical application papers,embossed papers & boards, envelope papers, manila envelope papers,facsimile paper, filter papers, fluorescent papers & boards, foldingboxboard, forest stewardship council (FSC) Papers, glassine papers,graphical boards, greaseproof papers, grey board, gummed papers,handmade papers & boards, inkjet papers, ivory boards, ivory papers,Kraft boards, Kraft lined chip, Kraft papers, Kraftliner, label papers,label papers (coated), label papers (uncoated), laid papers, laminates,laser printing papers (not copier), letter file, liquid packaging board,listing papers, long life papers & boards, lightweight coated paper(LWC), manila boards, manila envelopes, medical papers, metallizedpapers & boards, machine-finished (MF) papers, machine glazed (MG)bleached papers, MG papers, mini web reels, multi-layer boards, mediumweight coated (MWC) papers, near woodfree papers & boards, newsprint,recycled newsprint, OCR papers, offset papers, on-machine coated papers& boards, one-time carbon, packaging boards, packaging papers, partmechanical papers & boards, pen plotter & map papers, poster papers,preprint papers, pressboards, pulpboard, rag bank & bond papers, realart papers & boards, recycled boards, recycled coated paper & board,recycled graph.board(100% PCW), recycled graph.board(<100% PCW),recycled graph.paper(<100% PCW), recycled graphical paper (100% PCW),recycled papers, release papers, sack and Kraft Paper, SC gravure, SCoffset, security papers, self-adhesive base papers, self-adhesivepapers, silicone papers, solid bleached board, special coated paper,special surface papers & boards, stamp papers, stationery, syntheticpapers, tag papers & boards, testliner, textured papers & boards,thermal paper, thermal transfer papers, thin opaques/bible papers,ticket boards, tissue, translucent paper, tube papers & boards, ULWC,uncoated mechanical papers, vegetable parchment, wallpaper base,watermarked papers, web Offset reels, wet strength papers, WF bulkycoated papers & boards, WF envelope/cartridge, WF gloss coated papers &boards, WF gloss coated for dig.print, WF matt coated papers & boards,WF matt coated for dig.print, WF one side coated papers & boards, WFsatin coated papers & boards, WF silk coated papers & boards, WFuncoated papers & boards, white lined chipboard, and wove papers.

The paper article of the invention includes a natural fiber, a syntheticfiber, or a mixture thereof having a length of about 0.8 mm to about 5mm. If the fiber is less than about 0.8 mm, the fiber can break apartduring manufacturing. If the fiber is greater than about 5 mm, the fibercan aggregate during manufacturing to cause clumps in the resultingpaper article.

In some embodiments, the natural fiber is from a hardwood source, suchas, for example, oak, maple, and eucalyptus. In some embodiments whenthe fiber is from a hardwood source, the fiber is about 0.8 mm to about2 mm long. In some embodiments, the natural fiber is from a softwoodsource, such as, for example, pine, aspen, and birch. In someembodiments when the fiber is from a softwood source, the fiber is about2 mm to about 5 mm long. In some embodiments, the fiber is synthetic,such as, for example, a polyolefin, a polyester, or a cellulosic fiber(e.g., cellulose acetate and/or rayon).

The paper article of the invention can further include one or moreadditives commonly used in papermaking. Nonlimiting examples of usefuladditives include additional wet strength agents (e.g.,urea-formaldehyde resins, melamine formaldehyde resins,polyethyleneimine resins, polyacrylamide resins, polyvinylamine resins,dialdehyde starches, and derivatives thereof), dry strength additives(e.g., polysalt coacervates rendered water soluble by the inclusion ofionization suppressors, carboxylmethyl cellulose), debonders, whichincrease the softness of the paper webs (e.g., quaternary ammoniumchlorides such as ditallowdimethyl ammonium chloride andbis(alkoxy-(2-hydroxy)propylene) quaternary ammonium compounds),pigments, dyes, fluorescers, and the like. In some embodiments when thepaper article of the invention includes carboxymethyl cellulose (CMC),the CMC acts synergistically with the wet strength resin of theinvention and is present in an amount of about 0.1 wt. % to about 0.2wt. % for every 1 wt. % of wet strength resin.

The paper article of the invention can be single ply or multiple-ply(e.g., 2-ply, 3-ply, 4-ply, 5-ply, or 6-ply). It has a dry strength ofabout 300 g/in per ply to about 2000 g/in per ply, preferably about 500g/in per ply to about 1500 g/in per ply, more preferably about 700 g/inper ply to about 1200 g/in per ply, and a wet strength of about 60 g/inper ply to about 300 g/in per ply, preferably about 100 g/in per ply toabout 300 g/in per ply, more preferably about 140 g/in per ply to about240 g/in per ply. The paper article of the invention has a wet/drytensile ratio of about 10% to about 30%, preferably about 15% to about25%, for example, about 20%. The basis weight of the paper article ofthe invention is about 10 pounds per 30,000 square feet (lbs/30,000 ft²)to about 30 lbs/30,000 ft², for example, about 15 lbs/30,000 ft² toabout 28 lbs/30,000 ft². The wet strength of the paper article of theinvention can be determined by methods known to one skilled in the art,such as a suitable ASTM method. The dry strength of the paper article ofthe invention can be determined by methods known to one skilled in theart, such as a suitable ASTM method. The wet/dry tensile ratio of thepaper article of the invention can be determined by methods known to oneskilled in the art, such as a suitable ASTM method. The basis weight ofthe paper article of the invention can be determined by methods known toone skilled in the art, such as a suitable ASTM method.

The paper article of the invention can be formed by any method known toone skilled in the art. For example, a five step process for theformation of the paper of invention is described below (see, e.g., U.S.Pat. No. 4,637,859, incorporated herein by reference).

In the first step, an aqueous dispersion of papermaking fibers and thepolymer of Formula I is provided. Papermaking fibers useful in thepresent invention include bleached or unbleached cellulosic fiberscommonly known as wood pulp fibers. Fibers derived from soft woods(gymnosperms or coniferous trees) and hard woods (angiosperms ordeciduous trees) are contemplated for use in this invention. The woodpulp fibers can be produced from native wood by any pulping processknown to one skilled in the art. Chemical processes (e.g., sulfite,sulphate, soda processes), mechanical processes (e.g., thermochemical),semi-chemical, and semi-mechanical processes are suitable. Preferably,when the paper web of this invention is intended for use in absorbentproducts such as paper towels, bleached northern softwood Kraft pulpfibers are preferred. In addition to the various wood pulp fibers, othercellulosic fibers such as cotton linters, rayon, and bagasse can be usedin this invention. Synthetic fibers such as polyester and polyolefinfibers can also be used and, in fact, are preferred in certainapplications.

The second step includes forming an embryonic web of papermaking fibersfrom the aqueous dispersion provided in the first step. Any equipmentcommonly used in the art for dispersing fibers is appropriate. Thefibers are normally dispersed at a consistency of about 0.1% to about0.3% at the time an embryonic web is formed. Percent consistency isdefined as 100 times the quotient obtained when the weight of dry fiberin the system under discussion is divided by the total weight of thesystem. An alternative method of expressing moisture content of a systemsometimes used in the papermaking art is pounds of water per pound offiber or, alternatively and equivalently, kilograms of water perkilogram of fiber. The correlation between the two methods of expressingmoisture content can be readily developed. For example, a web having aconsistency of 25%, 50%, or 70%, comprises 3, 1, and 0.33 kilograms ofwater per kilogram of fiber, respectively. Fiber weight is alwaysexpressed on the basis of dry fibers.

The aqueous dispersion of papermaking fibers and embryonic web formedfrom the web can further include various additives commonly used inpapermaking Nonlimiting examples of useful additives include additionalwet strength agents (e.g., urea-formaldehyde resins, melamineformaldehyde resins, polyethyleneimine resins, polyacrylamide resins,and dialdehyde starches), dry strength additives (e.g., polysaltcoacervates rendered water soluble by the inclusion of ionizationsuppressors), debonders, which increase the softness of the paper webs(e.g., quaternary ammonium chlorides such as ditallowdimethyl ammoniumchloride and bis(alkoxy-(2-hydroxy)propylene) quaternary ammoniumcompounds), pigments, dyes, fluorescers, and the like.

Complete descriptions of useful wet strength agents can be found inTappi Monograph Series No. 29, Wet Strength in Paper and Paperboard,Technical Association of Pulp and Paper Industry (New York, 1965),incorporated herein by reference, and in other common references. Drystrength additives are described more fully in U.S. Pat. No. 3,660,338,incorporated herein by reference, and in other common references. Thelevels at which these materials are useful in paper webs is alsodescribed in the noted references. Specific debonders that can be usedin the present invention are described in U.S. Pat. Nos. 3,554,863,4,144,122, and 4,351,699, each incorporated herein by reference.

The resulting embryonic web is deposited onto a foraminous surface(i.e., the first foraminous member), and a portion of the aqueousdispersing medium is removed. As used herein, an “embryonic web” is aweb of fibers that is subjected to rearrangement on a deflection member.The fibers in the embryonic web normally comprise a relatively largequantity of water with typical consistencies in the range of about 5% toabout 25%, and is normally too weak to be capable of existing withoutthe support of an extraneous element, such as a Fourdrinier wire. At thetime the embryonic web is subjected to rearrangement on the deflectionmember, it must be held together by bonds weak enough to permitrearrangement of the fibers under the action of the deflection forces.

Any of the techniques known to those skilled in the papermaking art canbe used to form the embryonic web, and the precise method by which theembryonic web is formed is immaterial to the practice of this invention.Although batch process, such as handsheet making processes, can be used,continuous papermaking processes are preferred. Examples of saidprocesses are described, e.g., U.S. Pat. Nos. 3,301,746, and 3,994,771,each incorporated herein by reference.

The third step in the paper making process includes associating theembryonic web with a deflection member (i.e., the second foraminousmember) to bring the embryonic web into contact with the deflectionmember on which it will be subsequently deflected, rearranged, andfurther dewatered. The deflection member can include any physical formknown to one skilled in the art, such as an endless belt, a stationaryplate for use in making handsheets, or a rotating drum.

The deflection member must be foraminous. As used herein, “foraminous”is defined as possessing continuous passages connecting a first surface(i.e., upper surface, working surface, the surface with which theembryonic web is associated) with a second surface (i.e., lowersurface). The deflection member is constructed in such a manner that,when water removal from the embryonic web occurs, it can be dischargedfrom the system in the direction of the foraminous member without havingto again contact the embryonic web in either the liquid or the vaporstate. Water removal can occur by application of differential fluidpressure

The embryonic web-contacting surface of the deflection member can alsoinclude a macroscopically monoplanar, patterned, continuous networksurface, which defines within the deflection member a plurality ofdiscrete, isolated, deflection conduits. When a portion of the embryonicweb-contacting surface of the deflection member is placed into a planarconfiguration, the network surface is essentially monoplanar, meaningthat deviations from absolute planarity are tolerable, but notpreferred, as long as the deviations are not substantial enough toadversely affect the performance of the product formed on the deflectionmember. The network surface is said to be “continuous” because the linesformed by the network surface form at least one essentially unbrokennet-like pattern. The pattern is said to be “essentially” continuousbecause interruptions in the pattern are tolerable, but not preferred,as long as the interruptions are not substantial enough to adverselyaffect the performance of the product made on the deflection member. Thedeflection conduits are discrete and have a finite shape that depends onthe pattern selected for the network surface. The deflection conduitsare isolated because there is no connection within the body of thedeflection member between one deflection conduit and another. Thus,transfer of material from one deflection conduit to another is notpossible unless the transfer is effected outside the body of thedeflection member. An infinite variety of geometries for the networksurface and the openings of the deflection conduits are possible, andguidelines for selecting a particular geometry are described in U. S.Pat. No. 4,637,859.

The fourth step involves deflecting the fibers in the embryonic web intothe deflection conduits and removing water from the embryonic web, e.g.,by the application of differential fluid pressure to the embryonic web,to form an intermediate web of papermaking fibers. The deflecting iseffected under such conditions that there is essentially no waterremoval from the embryonic web through the deflection conduits after theembryonic web has been associated with the deflection member prior tothe deflecting of the fibers into the deflection conduits. At the timethe fibers are deflected into the deflection conduits or after suchdeflection, water removal from the embryonic web and through thedeflection conduits begins. The third and fourth steps essentially canbe accomplished simultaneously through the use of a technique analogousto the wet-microcontraction process used in papermaking. The waterremoval that occurs both during and after deflection results in adecrease in fiber mobility in the embryonic web, which tends to fix thefibers in place after they have been deflected and rearranged.

The fifth step includes drying the intermediate web to form the paperarticle of the invention. Any means known to one in the papermaking artcan be used to dry the intermediate web. For example, flow-throughdryers and Yankee dryers, alone and in combination, are satisfactory.Optionally, a predryer can be used.

Optionally, but preferably, the dried article is foreshortened followingthe first step of the paper making process. As used herein,“foreshortening” refers to the reduction in length of a dry paper webwhich occurs when energy is applied to the dry web to reduce the lengthof the web and to rearrange the fibers with an accompanying disruptionof fiber-fiber bonds. Foreshortening can be accomplished in any ofseveral well-known ways, such as creping (i.e., adhering the dried webto a surface and then removing it from that surface with a doctorblade). Other techniques for foreshortening paper webs includesubjecting the web to compaction between a hard surface and a relativelyelastic surface, as described in U.S. Pat. Nos. 2,624,245, 3,011,545,3,329,556, 3,359,156, and 3,630,837, each of which are incorporatedherein by reference, and microcreping, as described in U.S. Pat. Nos.3,260,778, 3,416,192, 3,426,405, and 4,090,385, each of which areincorporated herein by reference.

EXAMPLE Example 1 Preparation of Bio-Polyaminoamide Epichlorohydrin

About 225 g (2.18 mol) of bio-diethylenetriamine and 100 grams of wateris placed in a 3-necked flask equipped with a mechanical stirrer,thermometer, and condenser. To this is added 290 grams (2.0 mol) ofbio-adipic acid. After the acid has dissolved in the amine, the solutionis heated to 185-200° C. and held there for 1.5 hours. Then, vacuum froma water pump is applied to the flask during the period required for thecontents of the flask to cool to 140° C. following which 430 grams ofwater is added. The bio-polyamide solution contains 52.3% solids and hadan acid number of 2.1.

To 60 grams of this bio-polyamide solution in a round bottom flask isadded 225 grams of water. This solution is heated to 50° C. and 12.5grams of bio-epichlorohydrin is added dropwise over a period of 11minutes. The contents of the flask are then heated to 60-70° C. until ithas attained a Gardner viscosity of greater than E. Then 150 grams ofwater is added to the product, and it is cooled to 25° C. Eleven mL of10% HCl is then added to adjust the pH to 5.0. The product contains 9.0%solids and has a Gardner viscosity of C-D.

Example 2 Handsheet Preparation

Northern softwood kraft (NSK) dry lap is repulped by soaking indistilled water (25 bond dry grams (BDG) in about 500 mL of water for 1hour at ambient conditions). The slurry is added to a Tappi beaker thatcontains about 1500 mL of tap water pretreated with sodium thiosulfateantichlor (0.5 mL of a stock solution containing 86 g/L Na₂S₂O₃ requiredat 1 ppm AvCl₂). The pulp slurry disintegrates in about 10 minutes. Theslurry is then added to 17 L of dechlorinated tap water in aproportioner. A weigh sheet is then formed using 2.543 L of well-mixedslurry (1.3% consistency). This slurry is added to a deckle box, whichcontains 54 mL of dechlorinated tap water (giving 0.04% consistency).Formation is effected via vacuum filtration through a wire. The wetsheet is passed over a vacuum slit (2×) and a drum dryer (3×). Theproportioner pulp consistency is then adjusted to 1.0%, based on thebone dry weight of the sheet. The solution pH is adjusted as desired(e.g., pH 8) in both the proportioner and the deckle box. The PulpFiltration Rate (PFR) is then measured by methods known to one skilledin the art. A solution of polyaminoamide epichlorohydrin from Example 1(69.57 g of a 0.2% solution based on solids) is added to theproportioner and allowed to mix for about 5 minutes. The resulting 6handsheets are placed in a 105° C. oven for 5 min.

The handsheets are characterized by methods known to one skilled in theart. Tensile strength is measured on 1″×4″ sections using a Model 1122Instron controlled by a Hewlett-Packard 86B computer. Handsheet caliperis measured using a Thwing-Albert VIR Electronic Thickness Tester. Wetburst is evaluated using a Thwing-Albert Burst Tester. A 4″ squarehandsheet section is soaked briefly in distilled water prior toobtaining wet burst values. All handsheets are equilibrated in aconstant temperature-humidity room for 24 hours prior to testing.

Nitrogen levels in handsheets are determined by Kjeldahl analysisperformed at either Huffman Laboratories (Wheatridge, Colo.) or HazletonLaboratories (Madison, Wis.). The latter typically provided“micro-Kjeldahl” analyses. Nitrogen levels are related to the level ofpolyaminoamide epichlorohydrin from Example 1 by assuming an elementalnitrogen content of 12.8% in the polyaminoamide epichlorohydrin.

A fully extended polymer of Example 1 monomer unit has an estimatedsurface area of 50 Å² (based on Pauling interatomic distances). Themaximum surface area for 0.01 g of fully extended polymer from Example 1is calculated according to the following equation: 50 Å²×0.01 g/270g/mol×1 m²/10×10²⁰ Å²×6.02×10²³ molecules/mole m²/0.01g, which expressesthe potential surface area coverage of the polymer of Example 1 at 1%usage. One gram of unbeaten pulp has a surface area of about 1 m²accessible to a dye of surface area 141 Å². This increases to about 7 m²upon beating to the point where tensile levels off (about pfr 10).

Example 3 Paper Preparation

A pilot scale papermaking machine is obtained. The headbox is a fixedroof suction breast roll former and the Fourdinier wire is 33 by 30(filaments per centimeter) five-shed. The furnish comprises 100%northern softwood Kraft pulp fibers with about 4 kilograms of the wetstrength resin from Example 1 per 1000 kg bone dry fibers. Thedeflection member is an endless belt and is formed about a foraminouswoven element made of polyester and having 17 (MD) by 18 (CD) filamentsper centimeter in a simple (2S) weave. Each filament is 0.18 mm indiameter; the fabric caliper is 0.42 mm and it has an open area of about47%. The deflection member is about 1.1 mm thick. The blow-throughpredryer operates at a temperature of about 93° C. The Yankee drum dryerrotates with a surface speed of about 244 meters (800 feet) per minute.The paper web is wound on a reel at a surface speed of 195 meters (640feet) per minute. The consistency of the embryonic web at the time oftransfer from the Fourdinier wire to the deflection member is about 10%;and the consistency of the predried web at the time of impression of thecontinuous network surface into the web by the impression nip rollagainst the surface of the Yankee dryer is between about 60% and about70%. The imprinted web is adhered to the surface of the Yankee dryerwith polyvinyl alcohol adhesive and is creped therefrom with a doctorblade having an 81° angle of impact.

The dimensions and values disclosed herein are not to be understood asbeing strictly limited to the exact numerical values recited. Instead,unless otherwise specified, each such dimension is intended to mean boththe recited value and a functionally equivalent range surrounding thatvalue. For example, a dimension disclosed as “40 mm” is intended to mean“about 40 mm.”

Every document cited herein, including any cross referenced or relatedpatent or application, is hereby incorporated herein by reference in itsentirety unless expressly excluded or otherwise limited. The citation ofany document is not an admission that it is prior art with respect toany invention disclosed or claimed herein or that it alone, or in anycombination with any other reference or references, teaches, suggests ordiscloses any such invention. Further, to the extent that any meaning ordefinition of a term in this document conflicts with any meaning ordefinition of the same term in a document incorporated by reference, themeaning or definition assigned to that term in this document shallgovern.

While particular embodiments of the present invention have beenillustrated and described, it would be obvious to those skilled in theart that various other changes and modifications can be made withoutdeparting from the spirit and scope of the invention. It is thereforeintended to cover in the appended claims all such changes andmodifications that are within the scope of this invention.

1. A polymer of Formula I:

wherein A is Cl, Br, OH, NO₃, or BF₄; each W independently is (CH₂)₁₋₈or

each Y independently is (CH₂)₁₋₈ or

each R¹ independently is H,

and each R² is H; or R¹ and R² together with the nitrogen to which theyare attached form with

the proviso that about 20 mole percent to about 40 mole percent of R¹are H; each R³ independently is H or OH; p is 1-8; each q independentlyis 0-8; wherein the molar ratio of W to Y is about 0.8:1 to about 1.4:1;and, wherein Formula I has a biobased content of at least about 95%. 2.The polymer of claim 1, wherein the biobased content is at least about97%.
 3. The polymer of claim 2, wherein the biobased content is at leastabout 99%.
 4. The polymer of claim 1, wherein each W independently is(CH₂)₁₋₈, each Y independently is (CH₂)₁₋₈, and p is 1-3.
 5. The polymerof claim 4, wherein each W independently is (CH₂)₂₋₄, and each Yindependently is (CH₂)₂₋₄.
 6. The polymer of claim 5, wherein A is Cl,each W independently is (CH₂)₄, each Y independently is (CH₂)₂, and pis
 1. 7. A method for synthesizing the polymer of claim 1, the methodcomprising: (a) reacting: (i)

having a biobased content of at least about 95%; and, (ii)

having a biobased content of at least about 95%; to form

having a biobased content of at least about 95%; and, (b)functionalizing the product from step (a) with

having a biobased content of at least about 95%, to form the polymer ofclaim 1; wherein each W independently is (CH₂)₁₋₈ or

each Y independently is (CH₂)₁₋₈ or

each Z independently is H or

each R³ independently is H or OH; p is 1-8; each q independently is 0-8;and, the molar ratio of W to Y is about 0.8:1 to about 1.4:1.
 8. Themethod of claim 7, wherein the biobased content of the polymer ofFormula I is at least about 97%.
 9. The method of claim 8, wherein thebiobased content of the polymer of Formula I is at least about 99%. 10.A paper article comprising a polymer of Formula I:

wherein A is Cl, Br, OH, NO₃, or BE₁; each W independently is (CH₂)₁₋₈or

each Y independently is (CH1)₁₋₈ or

each R¹ independently is H,

and each R² is H; or R¹ and R² together with the nitrogen to which theyare attached form

with the proviso that about 20 mole percent to about 40 mole percent ofR¹ are H. each R³ independently is H or OH; p is 1-8; each qindependently is 0-8; wherein the molar ratio of W to Y is about 0.8:1to about 1.4:1; and, Formula I has a bio-based content of at least about95%; and, wherein the paper has a dry strength of about 300 g/in per plyto about 2000 g/in per ply, and a wet strength of about 60 g/in per plyto about 400 g/in per ply.
 11. The article of claim 10, wherein thebiobased content of the polymer of Formula I is at least about 97%. 12.The article of claim 11, wherein the biobased content of the polymer ofFormula I is at least about 99%.
 13. The article of claim 10, whereineach W independently is (CH₂)₁₋₈, each Y independently is (CH₂)₁₋₈, andp is 1-3.
 14. The article of claim 13, wherein each W independently is(CH₂)₂₋₄, and each Y independently is (CH₂)₂₋₄.
 15. The article of claim14, wherein A is Cl, each W independently is (CH₂)₄, each Yindependently is (CH₂)₂, and p is
 1. 16. The article of claim 10,wherein the article comprises a natural fiber, a synthetic fiber, or amixture thereof.
 17. The article of claim 16, wherein the natural fiberis derived from a source selected from the group consisting of oak,maple, eucalyptus, pine, aspen, birch, and mixtures thereof.
 18. Thearticle of claim 16, wherein the synthetic fiber is selected from thegroup consisting of a polyolefin, a polyester, a cellulosic fiber, andmixtures thereof.
 19. The article of claim 10 further comprising anadditive selected from the group consisting of an additional wetstrength resin, a dry strength resin, a debonder, a pigment, a dye, afluorescer, and mixtures thereof.
 20. The article of claim 10, whereinthe article has a dry strength of about 500 g/in per ply to about 1500g/in per ply, and a wet strength of about 100 g/in per ply to about 300g/in per ply.
 21. The article of claim 10, wherein the article comprisesa basis weight of about 10 pounds per 30,000 square feet (lbs/ 30,000ft²) to about 30 lbs/30,000 ft².
 22. The article of claim 21, whereinthe basis weight is about 15 lbs/30,000 ft² to about 28 lbs/30,000 ft².23. The article of claim 10, wherein the article is single ply ormultiple-ply.
 24. The article of claim 10, wherein the article isselected from the group consisting of a towel, a tissue, and apaperboard.